EP1323680A1 - Method for recovering nitrates from percolating waters coming from solid urban waste materials - Google Patents

Method for recovering nitrates from percolating waters coming from solid urban waste materials Download PDF

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Publication number
EP1323680A1
EP1323680A1 EP20020027261 EP02027261A EP1323680A1 EP 1323680 A1 EP1323680 A1 EP 1323680A1 EP 20020027261 EP20020027261 EP 20020027261 EP 02027261 A EP02027261 A EP 02027261A EP 1323680 A1 EP1323680 A1 EP 1323680A1
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EP
European Patent Office
Prior art keywords
waters
nitrates
recovering
separating
percolating
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP20020027261
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German (de)
French (fr)
Inventor
Guido Vaccaro
Carlo Ferri
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ionics Italba SpA
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Ionics Italba SpA
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ionics Italba SpA filed Critical Ionics Italba SpA
Publication of EP1323680A1 publication Critical patent/EP1323680A1/en
Withdrawn legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/025Reverse osmosis; Hyperfiltration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/04Feed pretreatment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1268Membrane bioreactor systems
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2311/00Details relating to membrane separation process operations and control
    • B01D2311/04Specific process operations in the feed stream; Feed pretreatment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/444Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/06Contaminated groundwater or leachate
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • C02F3/302Nitrification and denitrification treatment
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Definitions

  • the present invention relates to a method for recovering nitrates from percolating waters coming from solid urban waste materials or a preset fraction thereof.
  • percolate materials which are generated from urban solid wastes, comprises a comparatively high concentration of ammonia and carbon, and cause at present a lot of problems for properly disposing of them.
  • the aim of the present invention is to overcome the above mentioned drawbacks, by providing a method for recovering nitrates from percolating water coming from urban solid wastes or a preselected fraction thereof, allowing to perform a process suitable to provide a product which can be used on waste composting masses, to reduce the bad odors therefrom, while allowing to provide a good quality water which can be used for several further applications.
  • a main object of the present invention is to provide such a method allowing to obtain a mixed composted material, having very high agronomic properties.
  • Yet another object of the present invention is to provide such a method which, owing to its specifically designed features, is very safe and reliable in operation.
  • Yet another object of the present invention is to provide such a method which can be managed in a simple and economic manner, thereby consequently optimizing all of the operating parameters of the method.
  • a method for recovering nitrates from percolating waters coming from urban solid waste or a preset fraction thereof characterized in that said method comprises the steps of subjecting said percolating waters to an aerobic process for nitrificating ammonia present in said waters and oxidating further organic materials in said waters, subjecting the processed waters to a further reverse osmosis process thereby separating a reusable permeate material and a nitrate-rich concentrate material.
  • the method according to the invention for recovering nitrates from percolating waters coming from solid urban waste materials or a preset fraction thereof comprises a step of performing a biologic process, in a full nitrification conditions, which is so carried out as to fully nitrificating ammonia and precursors thereof present in the percolated waters, so as to transform them into nitrates, while simultaneously oxidating the organic materials present in said waters.
  • the percolate materials which have been generally indicated at the block 1 in the accompanying drawings, are subjected to the oxidation and nitrification process by optionally using an ultrafiltering system for ultra-filtering the active sludges, said system being indicated at the reference number 2, in particular by using semipermeable membranes, immersed in the oxidating basins.
  • the ultrafiltering process would allow to separate the sludges directly in the oxidating basin, without the need of using a clarifying device arranged downstream of said oxidating basin.
  • the biologic treatment as shown, for example, in the schematic diagram of figure 3, can be performed in an active-sludge system 3, of any desired conventional types, with an oxidation of the residue materials, followed by a sludge settling and recirculating step.
  • an anaerobic system including a digestor 4, suitable to provide a great reduction of the organic materials, with development of biogas and with a consequent possibility of easily performing any power recovering operations.
  • an anaerobic processing system Downstream of the digestor device, in particular, an anaerobic processing system will be arranged.
  • the reverse osmosis system 6, in particular, owing to the applied pressure, will separate the processed water into a permeate, indicated by the reference number 7, comprising good quality clarified water, devoid of colloidal materials and bacteria, as well as organic substances, and into a concentrate 8 including all of the impurities.
  • the permeate material can be reused inside said system as service water, antifire system water and so on.
  • heavy metals would be present in the concentrate material from the reverse osmosis, then said heavy metals will be stripped or removed by a heavy metal stripping system 9, including conventional stripping means.
  • the reverse osmosis concentrate rich in nitrates, can be used for spraying composting waste piles or masses, as generally indicated at the reference number 10 in the accompanying drawings.
  • Said composting masses are subjected to a first step of aerating and moistening, to provide a degradation of the organic substances therein contained by aerobic microorganisms, while reducing the bad odor gaseous evolved substances.
  • Optimum contents of moisture as necessary for a microbic population suitable to metabolize the organic materials would be included in a 50-70% range.
  • the supplied nitrates will favor, in this operating step, greater nitrogen contents in the mixed composted material, thereby increasing their intrinsic agronomic value.
  • the invention provides a method eliminating the cost which will be necessary for disposing of the reverse osmosis concentrate material.
  • Said method moreover, allows to provide a mixed composted material, having high agronomic properties and allowing to produce very good quality water, while reducing the bad odors in the composting waste masses.
  • the used materials, as well as the contingent size and shapes of the system can be any depending on requirements.

Abstract

The present invention relates to a method for recovering nitrates from percolating waters coming from solid urban waste materials, or a preset fraction thereof, comprising the steps of subjecting said percolating waters to an aerobic process for oxidating the organic materials contained therein and for nitrificating ammonia and precursors thereof present in said waters, subjecting the processed waters to a further reverse osmosis process, for separating a re-usable permeate and a concentrate material rich in dissolved salts.

Description

    BACKGROUND OF THE INVENTION
  • The present invention relates to a method for recovering nitrates from percolating waters coming from solid urban waste materials or a preset fraction thereof.
  • As is known, percolate materials which are generated from urban solid wastes, comprises a comparatively high concentration of ammonia and carbon, and cause at present a lot of problems for properly disposing of them.
  • Such a disposal of procedure, involves a high disposal of cost, which negatively affect the managing of the process.
  • SUMMARY OF THE INVENTION
  • Accordingly, the aim of the present invention is to overcome the above mentioned drawbacks, by providing a method for recovering nitrates from percolating water coming from urban solid wastes or a preselected fraction thereof, allowing to perform a process suitable to provide a product which can be used on waste composting masses, to reduce the bad odors therefrom, while allowing to provide a good quality water which can be used for several further applications.
  • Within the scope of the above mentioned aim, a main object of the present invention is to provide such a method allowing to obtain a mixed composted material, having very high agronomic properties.
  • Yet another object of the present invention is to provide such a method which, owing to its specifically designed features, is very safe and reliable in operation.
  • Yet another object of the present invention is to provide such a method which can be managed in a simple and economic manner, thereby consequently optimizing all of the operating parameters of the method.
  • According to one aspect of the present invention, the above mentioned aim and objects, as well as yet other objects, which will become more apparent hereinafter, are achieved by a method for recovering nitrates from percolating waters coming from urban solid waste or a preset fraction thereof, characterized in that said method comprises the steps of subjecting said percolating waters to an aerobic process for nitrificating ammonia present in said waters and oxidating further organic materials in said waters, subjecting the processed waters to a further reverse osmosis process thereby separating a reusable permeate material and a nitrate-rich concentrate material.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • Further characteristics and advantages of the present invention will become more apparent hereinafter from the following detailed disclosure of a preferred, though not exclusive, embodiment of a method for recovering nitrates from percolating waters coming from solid urban waste materials or a preset fraction thereof, which is illustrated, by way of an indicative, but not limitative, example, in the accompanying drawings, where:
  • Figure 1 shows an operating diagram of the method including an active-sludge biologic system, provided with ultra filtering means;
  • Figure 2 shows a schematic diagram of a method by which is carried out a preliminarily anaerobic operating step;
  • Figure 3 illustrates a schematic diagram of a method performed in an active-sludge biologic system, provided with sludge settling means; and
  • Figure 4 illustrates a further schematic diagram of a method in which is carried out a preliminarily anaerobic operating step or operation.
  • DESCRIPTION OF THE PREFERRED EMBODIMENTS
  • With reference to the above mentioned figures, the method according to the invention for recovering nitrates from percolating waters coming from solid urban waste materials or a preset fraction thereof, comprises a step of performing a biologic process, in a full nitrification conditions, which is so carried out as to fully nitrificating ammonia and precursors thereof present in the percolated waters, so as to transform them into nitrates, while simultaneously oxidating the organic materials present in said waters.
  • The percolate materials, which have been generally indicated at the block 1 in the accompanying drawings, are subjected to the oxidation and nitrification process by optionally using an ultrafiltering system for ultra-filtering the active sludges, said system being indicated at the reference number 2, in particular by using semipermeable membranes, immersed in the oxidating basins.
  • The ultrafiltering process would allow to separate the sludges directly in the oxidating basin, without the need of using a clarifying device arranged downstream of said oxidating basin.
  • The biologic treatment, as shown, for example, in the schematic diagram of figure 3, can be performed in an active-sludge system 3, of any desired conventional types, with an oxidation of the residue materials, followed by a sludge settling and recirculating step.
  • Before the biologic treatment step, it would be possible to provide an anaerobic system including a digestor 4, suitable to provide a great reduction of the organic materials, with development of biogas and with a consequent possibility of easily performing any power recovering operations.
  • Downstream of the digestor device, in particular, an anaerobic processing system will be arranged.
  • Downstream of the active-sludge biologic aerobic system, which can be provided with means for separating the biomasses by settling or ultrafiltering, it would be moreover possible to provide a further settling and/or filtering step 11, before the inlet to the reverse osmosis system 6.
  • The reverse osmosis system 6, in particular, owing to the applied pressure, will separate the processed water into a permeate, indicated by the reference number 7, comprising good quality clarified water, devoid of colloidal materials and bacteria, as well as organic substances, and into a concentrate 8 including all of the impurities.
  • In particular, the permeate material can be reused inside said system as service water, antifire system water and so on.
  • If heavy metals would be present in the concentrate material from the reverse osmosis, then said heavy metals will be stripped or removed by a heavy metal stripping system 9, including conventional stripping means.
  • The reverse osmosis concentrate, rich in nitrates, can be used for spraying composting waste piles or masses, as generally indicated at the reference number 10 in the accompanying drawings.
  • Said composting masses, in particular, are subjected to a first step of aerating and moistening, to provide a degradation of the organic substances therein contained by aerobic microorganisms, while reducing the bad odor gaseous evolved substances.
  • Optimum contents of moisture as necessary for a microbic population suitable to metabolize the organic materials, would be included in a 50-70% range.
  • Thus, the required moistening of the organic waste masses would constitute per se a depurating system proper.
  • The supplied nitrates will favor, in this operating step, greater nitrogen contents in the mixed composted material, thereby increasing their intrinsic agronomic value.
  • Moreover, if anoxic pockets would be formed in said composting masses, then the spraying of nitrates would make oxygen available for the composting population, so as to greatly reduce the development of bad odors.
  • From the above disclosure it should be apparent that the invention fully achieves the intended aim and objects.
  • In particular, the invention provides a method eliminating the cost which will be necessary for disposing of the reverse osmosis concentrate material.
  • Said method, moreover, allows to provide a mixed composted material, having high agronomic properties and allowing to produce very good quality water, while reducing the bad odors in the composting waste masses.
  • The invention, as disclosed, is susceptible to several modifications and variations, all of which will come within the scope of the invention.
  • Moreover, all the process steps can be replaced by other technically equivalent process steps.
  • In practicing the invention, the used materials, as well as the contingent size and shapes of the system can be any depending on requirements.

Claims (8)

  1. A method for recovering nitrates from percolating waters coming from urban solid waste or a preset fraction thereof, characterized in that said method comprises the steps of subjecting said percolating waters to an aerobic process for nitrificating ammonia present in said waters and oxidating further organic materials in said waters, subjects the processed water to a further reverse osmosis process thereby separating a reusable permeate material and a nitrate-rich concentrate material.
  2. A method, according to the preceding claim, characterized in that said aerobic process is carried out in an active-sludge system with separating means and ultrafiltering means for separating and ultrafiltering the biomass being processed, by using semipermeable membranes either immersed or not in oxidating basins.
  3. A method, according to Claims 1 and 2, characterized in that said aerobic process is carried out in an active-sludge system having separating means for separating the biomass by settling and recirculating the sludge.
  4. A method, according to one or more of the preceding claims, characterized in that said method comprises an anaerobic processing step, carried out before the aerobic process or treatment, for reducing the organic materials and forming biogas.
  5. A method, according to one or more of the preceding claims, characterized in that said method further comprises the step of carrying out a settling and/or filtering step downstream of said aerobic processing step.
  6. A method, according to one or more of the preceding claims, characterized in that said method further comprises the step of subjecting the concentrate material deriving from the reverse osmosis to a stripping step for stripping heavy metals present in said concentrate material.
  7. A method, according to one or more of the preceding claims, characterized in that the concentrate material derived from said reverse osmosis is used for spraying composting waste masses.
  8. A method for recovering nitrates from percolating waters coming from solid urban waste materials, or a preset fraction thereof, and substantially as broadly disclosed and illustrated and for the intended aim and objects.
EP20020027261 2001-12-11 2002-12-06 Method for recovering nitrates from percolating waters coming from solid urban waste materials Withdrawn EP1323680A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ITMI20012610 2001-12-11
IT2001MI002610A ITMI20012610A1 (en) 2001-12-11 2001-12-11 PROCEDURE FOR THE RECOVERY OF NITRATES FROM PERCOLATION WATERS, COMING FROM SOLID URBAN WASTE OR FROM A PRE-SELECTED FRACTION

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EP1323680A1 true EP1323680A1 (en) 2003-07-02

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IT (1) ITMI20012610A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2300179A1 (en) * 2006-04-03 2008-06-01 C.P. Srl Control Of Pollution System for treatment of waste of food industry, includes obtaining concentrated brine with suitable characteristics for reutilization of waste for use in agriculture as organic amendment
EP2350400A1 (en) * 2008-09-10 2011-08-03 European Space Agency Instalation for the treatment of urea containing water, toilet, stable and method
ITVE20120025A1 (en) * 2012-07-16 2014-01-17 C P S R L Control Pollution PROCESS OF TREATMENT OF THE PERCOLATE COMING FROM LANDFILL OF SOLID URBAN WASTE.

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02164500A (en) * 1988-12-19 1990-06-25 Meidensha Corp Water purifying treatment apparatus
EP0413356A1 (en) * 1989-08-18 1991-02-20 Osaka Gas Co., Ltd. Process for treating waste water
WO1991007354A1 (en) * 1989-11-15 1991-05-30 Irving Ainsworth (Holdings) Limited Water treatment method
JPH04305287A (en) * 1991-04-01 1992-10-28 Kubota Corp Water treating equipment
JPH07232192A (en) * 1994-02-23 1995-09-05 Kubota Corp Treatment of sewage
US6146532A (en) * 1996-04-03 2000-11-14 Fraunhofer-Gesellschaft Zur Foerderung Der Angewandten Forschung E.V. Process for the biological purification of wastewater

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02164500A (en) * 1988-12-19 1990-06-25 Meidensha Corp Water purifying treatment apparatus
EP0413356A1 (en) * 1989-08-18 1991-02-20 Osaka Gas Co., Ltd. Process for treating waste water
WO1991007354A1 (en) * 1989-11-15 1991-05-30 Irving Ainsworth (Holdings) Limited Water treatment method
JPH04305287A (en) * 1991-04-01 1992-10-28 Kubota Corp Water treating equipment
JPH07232192A (en) * 1994-02-23 1995-09-05 Kubota Corp Treatment of sewage
US6146532A (en) * 1996-04-03 2000-11-14 Fraunhofer-Gesellschaft Zur Foerderung Der Angewandten Forschung E.V. Process for the biological purification of wastewater

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
PATENT ABSTRACTS OF JAPAN vol. 014, no. 427 (C - 0758) 13 September 1990 (1990-09-13) *
PATENT ABSTRACTS OF JAPAN vol. 017, no. 131 (C - 1036) 18 March 1993 (1993-03-18) *
PATENT ABSTRACTS OF JAPAN vol. 1996, no. 01 31 January 1996 (1996-01-31) *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2300179A1 (en) * 2006-04-03 2008-06-01 C.P. Srl Control Of Pollution System for treatment of waste of food industry, includes obtaining concentrated brine with suitable characteristics for reutilization of waste for use in agriculture as organic amendment
EP2350400A1 (en) * 2008-09-10 2011-08-03 European Space Agency Instalation for the treatment of urea containing water, toilet, stable and method
CN102203354A (en) * 2008-09-10 2011-09-28 欧洲航天局 Instalation for the treatment of urea containing water, toilet, stable and method
JP2012501848A (en) * 2008-09-10 2012-01-26 ヨーロピアン・スペース・エージェンシー Equipment, toilet, livestock shed and method for treatment of urea-containing water
CN102203354B (en) * 2008-09-10 2015-05-27 欧洲航天局 Instalation for the treatment of urea containing water, toilet, stable and method
ITVE20120025A1 (en) * 2012-07-16 2014-01-17 C P S R L Control Pollution PROCESS OF TREATMENT OF THE PERCOLATE COMING FROM LANDFILL OF SOLID URBAN WASTE.

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